EP3227470A1 - Corrosion inhibition - Google Patents
Corrosion inhibitionInfo
- Publication number
- EP3227470A1 EP3227470A1 EP15864760.2A EP15864760A EP3227470A1 EP 3227470 A1 EP3227470 A1 EP 3227470A1 EP 15864760 A EP15864760 A EP 15864760A EP 3227470 A1 EP3227470 A1 EP 3227470A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- moiety
- compound
- corrosion
- steel
- aliphatic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/04—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in markedly acid liquids
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/08—Anti-corrosive paints
- C09D5/082—Anti-corrosive paints characterised by the anti-corrosive pigment
- C09D5/086—Organic or non-macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
- C09D7/48—Stabilisers against degradation by oxygen, light or heat
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
- C09D7/60—Additives non-macromolecular
- C09D7/63—Additives non-macromolecular organic
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/54—Compositions for in situ inhibition of corrosion in boreholes or wells
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
- C23F11/14—Nitrogen-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
- C23F11/14—Nitrogen-containing compounds
- C23F11/141—Amines; Quaternary ammonium compounds
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
- C23F11/14—Nitrogen-containing compounds
- C23F11/149—Heterocyclic compounds containing nitrogen as hetero atom
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
- C23F11/16—Sulfur-containing compounds
- C23F11/165—Heterocyclic compounds containing sulfur as hetero atom
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2208/00—Aspects relating to compositions of drilling or well treatment fluids
- C09K2208/32—Anticorrosion additives
Definitions
- metal notably steel or an alloy steel
- metal notably steel or an alloy steel
- these include the protection of steel used in a subterranean borehole to access a hydrocarbon reservoir and, more particularly but not by way of limitation the protection of steel exposed to a corrosive aqueous acidic liquid, such as when steel tubing is used to convey a flow of acidic aqueous liquid.
- the technique of matrix acidizing involves deliberate exposure of borehole steel to acid. This operation may be performed with coiled tubing, which is run into a borehole and then used to convey acid down the borehole to the formation. When the matrix acidizing operation comes to an end, the steel casing in the borehole and the exterior of the coiled tubing can be exposed to so-called unspent acid flowing back with formation fluids that flow back towards the surface.
- Adsorbed inhibitor(s) may influence the rate of corrosion by one or more of several mechanisms: (i) by forming a physical barrier film which restricts the diffusion of species to/from the metal surface, (ii) by blocking anodic and/or cathodic reaction sites directly, (iii) by interacting with corrosion reaction intermediates adsorbed on the surface and (iv) by influencing the electrical double layer that forms at the metal/solution interface.
- Adsorption may comprise physi-sorption which is the result of electrostatic attractive forces between inhibiting organic ions or dipoles and the electrically charged surface of the metal. The surface charge of the metal is due to the electric field at the outer Helmholtz plane of the electrical double layer existing at the metal/solution interface.
- adsorption is by chemi- sorption, which takes place more slowly than electrostatic adsorption and with a higher activation energy.
- Chemi- sorption involves electron transfer from electron-rich sites within the structure of the inhibitor molecule(s) to vacant low energy orbitals in the metal.
- electron-rich sites within an inhibitor molecule are heteroatoms with lone pair(s) of electrons or are multiple bonds and aromatic rings so that covalent bonds have electrons in ⁇ -orbitals. Because activation energy is required, to bring about chemi-sorption, the extent of chemi- sorption and therefore the efficacy of corrosion inhibition may increase with temperature.
- Chemi-sorbed acetylenic compounds can react to form polymeric inhibitor films. Such reaction/polymerisation is surface-catalysed.
- Corrosion inhibitors are frequently marketed as a mixture containing materials which inhibit corrosion together with other materials which enhance inhibition, even though these other materials do not function as corrosion inhibitors (or are less efficacious) if used alone. In some cases these mixtures are proprietary and their exact composition is not made public.
- a mixture which contains a chemi-sorbing corrosion inhibitor may also include non-ionic or cationic surfactants to assist in solubilising other components in the mixture and/or to assist in deposition on the steel, quaternary nitrogen compounds, amines (which will protonate to quaternary nitrogen under acidic conditions) and organic solvent(s).
- Some oilfield corrosion inhibitor products are mixtures which make use of a synergistic combination of an amine and an acetylenic alcohol.
- the corrosion inhibiting effect of an inhibitor or corrosion inhibiting mixture can be tested in various ways.
- One direct method of testing is to use a test piece, which is a sample of the steel to be protected, customarily referred to as a "coupon".
- This coupon is exposed for a measured length of time to an acidic solution containing a known concentration of corrosion inhibitor.
- the loss in weight of the coupon is measured and expressed as weight loss per unit surface area.
- the coupon may also be examined for localised pitting and the extent of pitting may be expressed as a numerical value: the so-called pitting index.
- stainless steels are alloy steels containing chromium and nickel as the main alloying metals. Alloy steels may have a single phase, either ferrite or austenite, or may have two phases mingled together.
- PREN pitting resistance equivalent number
- PREN wt Cr + 3.3(wt Mo + 0.5(wt%W)) + *.wt%N where x is given as either 16 or 30.
- Duplex stainless steels are composed of a mixture of austenite and ferrite phases, most typically with each phase in the range 25-75vol . They may have either a ferrite matrix or an austenitic matrix. As shown by the following table, the specified compositions for a range of duplex stainless steels include molybdenum and sometimes include other alloying metals such as tungsten, manganese and copper.
- the duplex alloy 2205 contains 45-55vol austentite in a ferrite matrix, i.e. the ferrite is the continuous phase.
- the main alloying elements, chromium, molybdenum, nickel, manganese and nitrogen are not equally distributed in the two phases. Austentite is enriched in nickel, manganese and nitrogen whilst ferrite is enriched in chromium and molybdenum.
- the nickel-rich austenite phase is cathodic relative to the anodic ferrite matrix.
- Steel pipework and steel casing in a borehole are sometimes made of duplex stainless steel and are examples of duplex stainless steel which may be exposed to acidic solutions during well invention operations such as matrix acidizing treatments.
- Other alloy steels have a single phase, which may be ferritic or autenitic. Examples are given in the following table:
- cationic materials which chemi-sorb to a metal surface can give good initial corrosion protection, but can also de-sorb, and so may not remain on the metal surface after an initial exposure to the cationic material.
- compounds which are able to polymerise on the metal surface form a persistent films so that corrosion protection is long lasting.
- embodiments of the present disclosure provide further development of corrosion inhibitor compounds able to polymerise on the metal surface.
- a first aspect of the present disclosure is a compound containing at least one moiety (A) comprising at least one hetero atom which is nitrogen, oxygen, phosphorus or sulphur, and also at least one moiety (B) which contains one or more polymerisable groups containing at least one double or triple bonded carbon atom, with the moieties (A) and (B) directly or indirectly covalently connected together.
- Some embodiments of such a compound may be represented by a general formula A(m)-Y(p)-B(n) wherein Y denotes a covalent bond or a connecting moiety, and m, n and p each independently denote a value in a range from 1 to 10.
- a linking group Y may be an aliphatic, aromatic or mixed aliphatic and aromatic moiety.
- the present disclosure provides each of:
- An aqueous solution which may be an aqueous acidic solution, having dissolved or suspended therein a corrosion inhibiting amount of a compound according to the first aspect of this disclosure;
- a corrosion inhibiting composition which may be a liquid concentrate intended to be used as a corrosion inhibiting additive in an aqueous solution, containing a compound according to the first aspect of this disclosure and a carrier material which may be a carrier fluid;
- a method of inhibiting corrosion of a metal, which may be steel, exposed to aqueous solution comprising including a compound according to the first aspect of this disclosure in the aqueous solution.
- the method is a method of inhibiting corrosion of steel surfaces in a system exposed to an aqueous liquid, wherein the surfaces comprise at least two steels which differ in composition, i.e. differ qualitatively and/or quantitatively in the elements additional to iron which are present in the steel.
- the method is a method of inhibiting corrosion of duplex steel surfaces in a system exposed to an aqueous liquid,. The steel surfaces may then comprise at least two steels which differ in composition where at least one steel surface is a duplex steel.
- Aqueous solution containing a compound according to the first aspect of this invention may be acidic. It may possibly be a solution with pH below zero, as is the case with a solution used for matrix acidizing. Thus the corrosion inhibiting compound may be utilized in a matrix acidizing composition and procedure.
- a sub-structure constituting a moiety (A) may comprise an aliphatic, aromatic or mixed aliphatic/aromatic structure and then a heteroatom may:
- (iii) be attached to one or more aliphatic carbon atoms, for instance as in aliphatic amines and quaternary ammonium compounds.
- Each of these possibilities has the hetero atom attached to one or more carbon atoms by covalent bonds.
- a moiety (A) there may be more than one hetero atom in which case some hetero atoms may be in or attached to aromatic rings while others may be in aliphatic groups.
- the number of carbon atoms in a moiety (A) may possibly be at least three but not more than 25, possibly not more than 20.
- the ratio of carbon atoms to hetero atoms in a moiety (A) may possibly lie in a range from 2: 1 or 3: 1 up to 7: 1 or 10: 1.
- At least one heteroatom within a moiety (A) may be nitrogen. It is possible that a moiety (A) may contain a plurality of hetero atoms where at least some, perhaps a majority, of the hetero atoms are nitrogen whilst the remainder of the hetero atoms are oxygen, phosphorus or sulphur. It is also possible that a moiety (A) may contain a plurality of hetero atoms which are all nitrogen.
- a moiety (A) may enhance solubility in aqueous corrosive fluid and may promote or enhance adsorption and interaction on a range of different metal and alloy surfaces.
- a moiety (A) may therefore include functional groups which promote solubility and enhance physi- and/or chemi- sorption.
- additional substituents may be incorporated to increase solubility in the aqueous corrosive fluid and/or to promote adsorption on metal surfaces.
- a moiety (B) contains a group intended to polymerise with other polymerisable groups after adsorption onto a metal surface. It contains at least one aliphatic carbon atom with a double or triple bond. Examples are a carbon-carbon triple bond as in an acetylenic group, a carbon- nitrogen triple bond as in a cyano group and conjugated double bonds in a structure with an olefinic double bond conjugated to a keto group, as in an alpha- olefinic aldehyde or alpha- olefinic ketone structure.
- the number of carbon atoms in a moiety (B) may be at least three and possibly at least four or five.
- the number of carbon atoms in a moiety (B) may possibly be no more than 25, possibly no more than 18, 12 or even 6,
- moiety Y denotes a linking group containing at least three carbon atoms. This provides flexibility in the structure of the molecule, which allows the moiety B to polymerise more easily thus enhancing corrosion inhibition.
- moiety Y is a connecting group, it may contain a saturated carbon chain of at least three carbon atoms, providing some flexibility in the connection between moieties (A) and (B).
- a partially unsaturated chain may possibly incorporate at least two carbon-carbon single bonds.
- a linking carbon chain may incorporate an aromatic ring or rings.
- a corrosion inhibiting compound in accordance with this disclosure is used in a mixture with a second compound which comprises a moiety (B) (i.e. contains a polymerisable group) but does not contain a moiety (A).
- B a moiety
- A a moiety
- the second compound may comprise one or more polymerisable groups containing double or triple bonded carbon.
- the second com ound comprises one or more polymerisable
- the second compound has a molecular weight which is smaller than that of the first compound.
- a process is terminated when its operations are completed, but could have additional steps not included in the figure.
- a process may correspond to a method, a function, a procedure, a subroutine, a subprogram, etc.
- a process corresponds to a function
- its termination corresponds to a return of the function to the calling function or the main function.
- the term “storage medium” may represent one or more devices for storing data, including read only memory (ROM), random access memory (RAM), magnetic RAM, core memory, magnetic disk storage mediums, optical storage mediums, flash memory devices and/or other machine readable mediums for storing information.
- ROM read only memory
- RAM random access memory
- magnetic RAM magnetic RAM
- core memory magnetic disk storage mediums
- optical storage mediums flash memory devices and/or other machine readable mediums for storing information.
- computer- readable medium includes, but is not limited to portable or fixed storage devices, optical storage devices, wireless channels and various other mediums capable of storing, containing or carrying instruction(s) and/or data.
- embodiments may be implemented by hardware, software, firmware, middleware, microcode, hardware description languages, or any combination thereof.
- the program code or code segments to perform the necessary tasks may be stored in a machine readable medium such as storage medium.
- a processor(s) may perform the necessary tasks.
- a code segment may represent a procedure, a function, a subprogram, a program, a routine, a subroutine, a module, a software package, a class, or any combination of instructions, data structures, or program statements.
- a code segment may be coupled to another code segment or a hardware circuit by passing and/or receiving information, data, arguments, parameters, or memory contents. Information, arguments, parameters, data, etc. may be passed, forwarded, or transmitted via any suitable means including memory sharing, message passing, token passing, network transmission, etc.
- first and second features are formed in direct contact
- additional features may be formed interposing the first and second features, such that the first and second features may not be in direct contact.
- the present disclosure is concerned with multifunctional compounds and their use as corrosion inhibitors in a corrosive solution, in particular in a corrosive acidic aqueous solution.
- Surfaces to be protected from corrosion will ordinarily be metallic and the metal may be an alloy.
- surfaces to be protected may be steel and the steel may be single phase or duplex alloy steel.
- the efficacy of a mixture is dependent on the proportions in which its constituents deposit on the metal surfaces to be protected. There can be significant heterogeneity in deposition if the metal has more than one phase and the protective inhibitor film may form at different rates on the different exposed phases of the metal micro structure.
- the result is that a particular inhibitor formulation provides adequate protection on certain metals but the same formulation provides only a very limited (non-optimum) protection on other metals. This can be a major disadvantage when carrying out an operation which requires that a corrosive fluid contacts several different metals.
- a mixture might contain both a compound R -A and a compound R 2 -B, wherein A and B may be moieties as defined in the summary above. If such a mixture is used to inhibit corrosion of a metal surface, it is possible that the extent of adsorption will be affected by (i) overall preferential adsorption of one of the molecules relative to the other, (ii) phase-specific adsorption of one or both of the molecules on different micro structural phases of the metal and/or (iii) coadsorption of Ri-A and R 2 -B at an overall molar ratio which is different to the ratio provided in the mixture and which is non-optimum in terms of inhibition performance.
- a polymerisable group B might display strong preferential absorption on austenitic steel with poor absorption on another steel or alloy steel or vice versa, leading to poor overall inhibition of corrosion.
- Such segregated adsorption and co-adsorption behaviour will depend on the physico-chemical properties of the metal surface and the various micro structural phases exposed on that surface. Therefore, the degree and exact nature of this behaviour will be different on different metal surfaces with the possible consequence that there is inadequate corrosion protection for some of the metals which are exposed to the corrosive solution.
- multi-functional inhibitor molecules in which moieties (A) and (B) are parts of a single molecule provide a way to deliver desired functional groups to the surface of a broader range of metal surfaces and provide a way to control directly the molar ratio of functional groups in the adsorbed inhibitor film.
- Multifunctional inhibitor molecules can be used to provide improved corrosion protection when applied on a broader range of metals as compared to the use of the same concentration of functional groups presented to the metal surfaces as a mixture of separate molecules.
- a general formula may be written as A(m)-Y(p)-B(n) wherein Y denotes a covalent bond or a connecting moiety, and m, n and p each independently denote a value in a range from 1 to 10. It will be appreciated that if A, Y and B all contain carbon atoms which are connected covalently, there may be more than one possibility for the choice of boundaries between moieties (A) and (B) and a connecting moiety Y between them.
- a moiety (A) which has an organic (ie carbon-based) structure may be aromatic, aliphatic or mixed aromatic and aliphatic. It incorporates at least one hetero atom.
- a moiety (A) may enhance solubility in aqueous solution because the presence of the hetero atom or atoms gives polarity within the molecule.
- the presence of the hetero atom or atoms may also assist physi- sorption or chemi- sorption onto a metallic surface.
- a moiety (A) may have a hetero atom within an aromatic ring or may have a hetero atom directly attached to an aromatic ring so that the hetero atom can participate in the delocalised bonding of the aromatic ring. It is also possible that a moiety (A) may have a hetero atom in an aliphatic group. It will be appreciated that each of these possibilities has the hetero atom or atoms attached to the organic structure of the (A) moiety through one or more covalent bonds.
- a moiety (A) there may be more than one hetero atom, in which case at least one hetero atom may be within or attached to an aromatic ring while at least one further hetero atom may be in an aliphatic group.
- the number of carbon atoms maybe at least twice the number of hetero atoms but possibly not more than 10 times the number of hetero atoms. If a moiety (A) contains more than one aliphatic or aromatic ring, these may be separate rings connected together or may be in a fused ring system. In either case the ratio of rings to hetero atoms may lie in a range from 2: 1 to 1:2, possibly from 2: 1 to 1: 1.
- Some embodiments of moiety (A) have a fused ring system with at least one hetero atom in an aromatic ring and at least one further hetero atom in an aliphatic substituent group on an aliphatic ring.
- a moiety (A) contains at least one hetero atom which is nitrogen.
- nitrogen atom(s) may be permanently cationically charged (e.g. as in N-alkyl substituted pyridinium structures and alkyl quaternary ammonium structures) or may be protonatable under acid conditions (e.g. as in amine-substituted aromatic ring structures and alkyl amines).
- Cationically charged nitrogen atom(s) both enhance solubility in the corrosive fluid and promote adsorption on a metal surface.
- the anion which is present may be a halide shown as X " , which may be CI " , Br " or ⁇ .
- Iodide may be chosen because it is known that the presence of iodide anions enhances the adsorption of compounds containing cationic N atom(s) and/or N atoms which protonate under acid conditions.
- R 1; R 2 and R are linear or branched saturated or partially unsaturated alkyl chains with or without additional substituents such as hydroxyl groups.
- R 1; R 2 and R 3 can be the same or different.
- Ri is a linear dodecyl chain and exemplary R 2 and R 3 are methyl, ethyl or hydroxyethyl groups.
- a moiety (B) contains a polymerisable functional group.
- Such groups are capable of polymerisation with other such groups after deposition on the metal surface and this enables the molecules to combine together as a protective film.
- a polymerisable group may be one or more of
- moiety B contains a polymerisable group which is a -C(OH)-C ⁇ CH, i.e. a terminal alkyne with a hydroxyl group linked to the cc-carbon atom, also referred to as a propargyl group.
- a compound may contain more than one moiety (B) and hence more than one polymerisable functional group.
- the more than one polymerisable functional groups may be identical to each other, or they may be different.
- a broad range of aromatic amines can be functionalized with B-Y where sub- structure B is - C(OH)-C ⁇ CH.
- This broad range of aromatic amines includes 1,5-diamino-naphthalene, 9- amino-acridine, 1,4-diamino-anthraquinone, pararosaniline, and 3,8-diamino-5-ethyl-6- phenylphenanthridinium chloride.
- functionalized aromatic amines where sub-structure B is -C(OH)-C ⁇ CH are given below:
- N-containing aromatic organic compounds are also candidates for B- Y-functionalization.
- tryptamine which has the structural formula: which incorporates two nitrogen atoms, one external and one internal with respect to the aromatic hydrocarbon ring structure.
- B-Y-derivatives of tryptamine are :
- the purine structure consists of a pyrimidine ring fused to an imidazole ring.
- the purine family includes purine, adenine, guanine, hypoxanthine, xanthine, theobromine, caffeine, uric acid and isoguanine.
- Tri(but-l-yn-3-ol)oleylammonium chloride and mono(but-l-yn-3-ol)di(hydroxyethyl) oleylammonium chloride each incorporate a hydrophobic oleyl group.
- B-Y- derivatives of aliphatic amines wherein B is -C(OH)-C ⁇ CH are given below. These structures protonate under acid conditions leading to enhanced solubility in the corrosive fluid and enhanced adsorption on metal and alloy surfaces.
- inhibitor compound in which moiety B contains a terminal alkyne functional group are:
- XI to XVI incorporate two different Y-groups, viz. -CH 2 - in structures XI, XIV, XV and XVI and -0-CH 2 - in structures XII and XIII.
- Related compounds could have a Y group which is a linear or branched hydrocarbon chain with 2-10 carbon atoms although longer chains are possible.
- a polymerisable group in moiety B may be an a-alkenyl ketone group.
- a compound containing such a group may conform to a general formula
- ketone function is directly linked to an aromatic ring in moiety (A) and the Ri group is typically -CH 2 OH or -CH 2 OCH 3 .
- the metal which is protected from corrosion by compound according to this disclosure may be steel or an alloy steel.
- An alloy steel may contain nickel, chromium, molybdenum and possibly other alloying metals.
- a compound according to this disclosure is included in an inhibitor composition which is used to protect a system in which there are a plurality of metals which come into contact with corrosive aqueous acidic liquid.
- the metals may be steel or steel alloys and they may be located within a subterranean borehole.
- Ethyl 6-bromohexanoate (7.42g, 33mmol) was dissolved in toluene (100ml) and cooled to -70°C and 1M diisobutylaluminium hydride (1M in toluene (30ml)) added over 15min and the reaction maintained at -75°C ⁇ 5°C for 1.5hr.
- Ethynyl magnesium bromide (0.5M in THF) (100ml) was added over 20min, the cooling bath removed and the mixture stirred for 3.5hr. The mixture was quenched with NH 4 C1 (aq) (150ml) and de-ionised water (150ml) at 0°C and filtered through celite®.
- the aqueous phase was extracted with diethyl ether.
- the combined organic phases were extracted with de-ionised water and brine, dried over sodium sulfate and the solvent removed.
- the product was purified by column chromatography eluting with 15-20% diethyl ether in hexane to give 8-bromo-l-octyn-3-ol, 4g (58% yield).
- Phenanthridine (1.76g, 9.82mmol) and 8-bromo-l-octyn-3-ol (2.02g, 9.8mmol) were added to acetonitrile (40ml) and heated at reflux for 48hr, then stirred at ambient temperature for 72hr.
- 6-Hydroxnaphthalene (823mg, 5.67mmol), 8-bromo-l-octyn-3-ol (1.16g, 5.65mmol) and anhydrous potassium carbonate (4g,) were added to acetone (30ml) and heated at reflux for 16hr; during which time the solvent was allowed to evaporate. The reaction was cooled, dichloromethane was added, the resulting solid was filtered off and washed with dichloromethane. The filtrate was concentrated and the residue was purified by column chromatography eluting with 30-50% ethyl acetate/hexane to give 8-(pyridin-3-yloxy)oct-l-yl-3- ol, 1.41g (92% yield).
- Tributylamine (930mg 5.2mmol) and 8-bromo-l-octyn-3-ol (520mg, 2.53mmol) were added to acetonitrile (1ml) and heated at reflux for 24hr.
- the reaction was cooled, diethyl ether added to give an oily precipitate.
- the solvent was decanted; diethyl ether was added to give a solid.
- the solid was filtered off and washed with diethyl ether and to give N,N,N-tributyl-6-hydroxyoct-7- yn-l-aminium bromide, 520mg (52% yield).
- HS80 a low carbon steel used to fabricate coiled tubing.
- 13Cr80 an alloy steel containing chromium without nickel, used to fabricate borehole casing;
- 22Crl25 also designated 2205, a duplex alloy steel which is an iron-chromium-nickel- molybdenum alloy, also used to fabricate casing.
- the corrosion inhibiting mixture was 0.3wt NMQCl accompanied by 0.1 wt cinnamonitrile and 0.5wt of polyoxyethylene tridecyl alcohol, which is a nonionic surfactant.
- the corrosion rate remained below 0.00161b/ft 2 /hour (7.8gm/m 2 /hour) throughout the six hour period. This was attributed to formation of a protective film through polymerisation of the cinnamonitrile after adsorption to the metal surface.
- the corrosion inhibitor was oct-l-yn-3-ol which is a hydrophobic acetylenic alcohol which is currently used as a corrosion inhibitor. In some others of these tests the inhibitor was a mixture containing oct-l-yn-3-ol together with C 1 3H27(OCH 2 CH 2 )ioOH which is a non-ionic surfactant. In some of the tests the corrosion inhibitor was propynlNMQCl which is compound XII on page 27.
- the concentrations of corrosion inhibitor and the results, expressed as weight loss per unit area, are set out in the following table.
- the coupons were also assessed for pitting index, which is a grading according to the extent of pitting.
- Oct-l-yn-3-ol has a polymerisable group but has low water solubility.
- the results in the table above show that even with the non-ionic surfactant present, corrosion protection was poor.
- Compound XII which contained an NMQCl moiety covalently attached to a polymerisable acetylenic group gave much better corrosion protection. This was attributed to the presence of the NMQCl moity in the molecule enabling adsorption on the steel surface, after which a protective film could be formed by polymerisation. When compound XII was used together with oct-l-yn-3-ol there was further reduction in corrosion, as shown by the bottom two rows of the table.
- N-propynyl quinolinium bromide (XI) [propynylQBr]
- XI N-propynyl quinolinium bromide
- a number of multifunctional inhibitor compounds were tested using coupons of 22Crl25 duplex alloy steel in the weight loss procedure used in Example 2 above. These multifunctional inhibitors are named in the table below and are compounds with preparations given above. Also included are the results from a comparative test using l-octyn-3-ol. In each test the concentration of corrosion inhibitor in the hydrochloric acid was 11 millimolar.
- the multifunctional compounds all resisted corrosion better than the comparative compound l-octyn-3-ol.
- the performance of such multifunctional compounds can be enhanced further by their usage in mixtures with polymerisable inhibitors such as acetylenic alcohols.
- Weight loss tests were carried out as in the previous example, using mixtures of the multifunctional inhibitor l-(6-hydroxyoct-7-ynyl)quinolinium bromide (II) and l-Octyn-3-ol.
- the overall concentration of corrosion inhibitor was l lmM in each test. The results are in the following table:
- the reduced weight loss indicates that there is synergy when the two materials are used in a mixture. This was attributed to the l-octyn-3-ol copolymerising with the deposited multifunctional compound and improving the coverage of the metal surface because the 1-octyn- 3-ol is a smaller molecule than the multifunctional compound.
- Example 6 In this example, a pretreatment step is carried out before a longer period in which steel is exposed to an acidic solution.
- Weight loss tests as in Example 2 above were carried out by a modified procedure.
- a first stage the coupons were exposed to a composition intended to deposit a protective film on the test coupons or (as a control) to an acidic solution without inhibitor.
- This pretreatment stage referred to as the film-forming stage (FFS)
- FFS film-forming stage
- the weight loss test was then carried out as in Example 2 above, using an acidic solution for 3 hours.
- This second stage is referred to as the film maintenance (FM) stage and the acidic solution contained a reduced concentration of corrosion inhibitor.
- FM film maintenance
- the subsequent film maintenance stage was carried out for 3 hours at 78°C using 4 mol/L hydrochloric acid containing oct-l-yn-3-ol at a concentration of either 2mmol/litre or 0.2 mmol/litre and also 0.5wt of the non-ionic surfactant C 13 H 27 (OCH 2 CH 2 ) 10 OH in each case.
- the maintenance stage was also carried out using coupons which had not received the film-forming treatment.
- the weight loss (WL) and pitting index (PI) results are in the following table:
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Wood Science & Technology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1421656.8A GB2532990A (en) | 2014-12-05 | 2014-12-05 | Corrosion inhibition |
PCT/US2015/056144 WO2016089487A1 (en) | 2014-12-05 | 2015-10-19 | Corrosion inhibition |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3227470A1 true EP3227470A1 (en) | 2017-10-11 |
EP3227470A4 EP3227470A4 (en) | 2018-12-19 |
Family
ID=52425511
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP15864760.2A Pending EP3227470A4 (en) | 2014-12-05 | 2015-10-19 | Corrosion inhibition |
Country Status (6)
Country | Link |
---|---|
US (1) | US10787745B2 (en) |
EP (1) | EP3227470A4 (en) |
BR (1) | BR112017011894A2 (en) |
GB (1) | GB2532990A (en) |
SA (1) | SA517381670B1 (en) |
WO (1) | WO2016089487A1 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2543498A (en) | 2015-10-19 | 2017-04-26 | Schlumberger Holdings | Corrosion inhibition |
EP3395800B1 (en) * | 2017-04-26 | 2021-11-03 | Henkel AG & Co. KGaA | Heterocyclic quaternary nitrogen compounds comprising a polymeric substituent and their use as a photolatent catalyst in curable compositions |
US11505733B2 (en) | 2019-04-16 | 2022-11-22 | Schlumberger Technology Corporation | Aqueous acidic compositions with a corrosion inhibitor |
CN110699677B (en) * | 2019-10-21 | 2022-07-15 | 威海海洋生物医药产业技术研究院有限公司 | Self-assembled film of methylacridine salt on carbon steel surface and corrosion resistance |
US20230365814A1 (en) * | 2022-05-11 | 2023-11-16 | Saudi Arabian Oil Company | Corrosion inhibitor solutions and corrosion-resistant substrates that include pyridinium hydroxyl alkyl ether compounds and methods of making the same |
Family Cites Families (59)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2935474A (en) * | 1955-11-28 | 1960-05-03 | Visco Products Co | Process of inhibiting corrosion and corrosion inhibiting compositions |
US3081304A (en) * | 1959-10-29 | 1963-03-12 | Gen Mills Inc | Amino hydroxy nitriles |
US3337470A (en) * | 1964-04-15 | 1967-08-22 | Air Reduction | Corrosion inhibition with propargyl cyclohexylamine |
US3335090A (en) * | 1964-04-15 | 1967-08-08 | Air Reduction | Corrosion inhibition with propargyl benzylamine |
GB1365291A (en) | 1970-09-25 | 1974-08-29 | Ici Ltd | Inhibition of corrosion |
GB1417555A (en) * | 1972-03-08 | 1975-12-10 | Ici Ltd | Inhibition of corrosion |
GB1434354A (en) * | 1972-08-17 | 1976-05-05 | Ici Ltd | Inhibition of corrosion |
US3816322A (en) | 1972-10-02 | 1974-06-11 | Dow Chemical Co | Corrosion inhibitor |
US4026807A (en) * | 1974-08-09 | 1977-05-31 | Petrolite Corporation | Alkynoxymethyl amines |
US4028268A (en) * | 1975-12-03 | 1977-06-07 | Exxon Research And Engineering Company | High temperature corrosion inhibitor |
EP0080794A1 (en) * | 1981-09-14 | 1983-06-08 | Gaf Corporation | Corrosion inhibitors containing N,N,1-trisubstituted prop-2-ynyl amines |
US4387041A (en) * | 1981-09-14 | 1983-06-07 | Gaf Corporation | Corrosion inhibitors |
US4760064A (en) | 1984-12-18 | 1988-07-26 | Otsuka Pharmaceutical Co., Ltd. | Carbostyril compounds, compositions containing same and processes for preparing same |
DE3681378D1 (en) * | 1985-08-14 | 1991-10-17 | Pumptech Nv | METHOD AND COMPOSITION FOR INHIBITING CORROSION OF IRON AND STEEL. |
US5120471A (en) | 1985-08-14 | 1992-06-09 | Dowell Schlumberger Incorporated | Process and composition for protecting chrome steel |
US4734259A (en) * | 1985-11-22 | 1988-03-29 | Dowell Schlumberger Incorporated | Mixtures of α,β-unsaturated aldehides and surface active agents used as corrosion inhibitors in aqueous fluids |
US4839368A (en) | 1986-05-02 | 1989-06-13 | Mochida Pharmaceutical Co., Ltd. | 1-acyl-2,3-dihydro-4(1H)-quinolinone-4-oxime derivatives |
US4880907A (en) | 1986-07-17 | 1989-11-14 | Exxon Research And Engineering Company | Quaternary salts of quinoline oligomer as metal surface protective materials (C-2212) |
US4698168A (en) | 1986-08-29 | 1987-10-06 | Hughes Tool Company | Corrosion inhibitor for well acidizing treatments |
US5096618A (en) | 1987-02-12 | 1992-03-17 | Dowell Schlumberger Incorporated | Process and composition for inhibiting high-temperature iron and steel corrosion |
US4946849A (en) | 1989-10-10 | 1990-08-07 | Flow Incorporated | Method for the treatment of malaria |
US5158693A (en) | 1991-08-29 | 1992-10-27 | Exxon Research And Engineering Co. | Oligoquinolinium metal oxide salts as sulfur corrosion inhibitors |
WO1994004504A1 (en) | 1992-08-19 | 1994-03-03 | Otsuka Pharmaceutical Co., Ltd. | Apoptosis regulator |
US5591381A (en) | 1992-10-22 | 1997-01-07 | Halliburton Company | Corrosion inhibiting compositions and methods |
TW448161B (en) | 1994-07-14 | 2001-08-01 | Otsuka Pharma Co Ltd | Cyclic amide derivatives |
US5697443A (en) | 1996-02-09 | 1997-12-16 | Halliburton Energy Services, Inc. | Method and composition for acidizing subterranean formations utilizing corrosion inhibitor intensifiers |
US5763368A (en) | 1996-05-30 | 1998-06-09 | Halliburton Energy Services, Inc. | Corrosion inhibited well acidizing compositions and methods |
EP0869258A1 (en) | 1997-04-03 | 1998-10-07 | Halliburton Energy Services, Inc. | Method and composition for acidizing subterranean formations utilizing corrosion inhibitor intensifiers |
US5756004A (en) | 1997-05-13 | 1998-05-26 | Halliburton Energy Services, Inc. | Quaternary ammonium compounds useful for inhibiting metal corrosion |
US5976416A (en) | 1997-05-13 | 1999-11-02 | Halliburton Energy Services, Inc. | Corrosion inhibited organic acid compositions and methods |
JP3510796B2 (en) | 1998-07-24 | 2004-03-29 | 朝日化学工業株式会社 | Corrosion inhibitor for acid cleaning of metal, cleaning liquid composition containing the same, and method of cleaning metal using the same |
US6281172B1 (en) | 1999-04-07 | 2001-08-28 | Akzo Nobel Nv | Quaternary nitrogen containing amphoteric water soluble polymers and their use in drilling fluids |
MXPA02003175A (en) | 1999-09-25 | 2002-09-30 | Smithkline Beecham Plc | Piperazine derivatives as 5 ht1b antagonists. |
GB0028702D0 (en) | 2000-11-24 | 2001-01-10 | Novartis Ag | Organic compounds |
US20050228016A1 (en) | 2002-06-13 | 2005-10-13 | Enrique Michelotti | Tetrahydroquinolines for modulating the expression of exogenous genes via an ecdysone receptor complex |
TW200503994A (en) | 2003-01-24 | 2005-02-01 | Novartis Ag | Organic compounds |
US7087554B2 (en) | 2003-04-10 | 2006-08-08 | Halliburton Energy Services, Inc. | Drilling fluids with improved shale inhibition and methods of drilling in subterranean formations |
US20050123437A1 (en) | 2003-12-03 | 2005-06-09 | Cassidy Juanita M. | Methods and compositions for inhibiting metal corrosion |
US7216710B2 (en) | 2004-02-04 | 2007-05-15 | Halliburton Energy Services, Inc. | Thiol/aldehyde corrosion inhibitors |
WO2006035954A1 (en) | 2004-09-28 | 2006-04-06 | Otsuka Pharmaceutical Co., Ltd. | Carbostyril compound |
ES2273581B1 (en) | 2005-06-23 | 2008-02-01 | Kao Corporation, S.A. | CORROSION INHIBITOR FOR ACIDS. |
JP5191155B2 (en) | 2006-03-27 | 2013-04-24 | 大塚製薬株式会社 | Medicaments comprising carbostyril compounds |
EP2053920B1 (en) | 2007-01-26 | 2014-04-30 | North Carolina State University | Inhibition of bacterial biofilms with imidazole derivatives |
US20080308770A1 (en) | 2007-06-14 | 2008-12-18 | Laxmikant Tiwari | Mono and bis-ester derivatives of pyridinium and quinolinium compounds as environmentally friendly corrosion inhibitors |
US8288410B2 (en) | 2008-07-08 | 2012-10-16 | Florida Agricultural And Mechanical University | 3-substituted quinolinium and 7H-indolo[2,3-c]quinolinium salts as new antiinfectives |
US7902124B2 (en) * | 2008-08-29 | 2011-03-08 | Schlumberger Technology Corporation | Self-diverting acid treatment with formic-acid-free corrosion inhibitor |
US7994099B2 (en) * | 2009-04-14 | 2011-08-09 | Haliburton Energy Services, Inc. | Corrosion inhibitor compositions comprising an aldehyde and a thiol and/or an amine functionalized ring structure and associated methods |
CN101892042B (en) * | 2010-06-30 | 2013-03-20 | 中国海洋石油总公司 | High temperature acidizing corrosion inhibitor and preparation method thereof |
CN102049213B (en) * | 2010-11-12 | 2013-06-19 | 西华师范大学 | Propargyl alcohol type quaternary ammonium salt surfactant and preparation method thereof |
US8236204B1 (en) | 2011-03-11 | 2012-08-07 | Wincom, Inc. | Corrosion inhibitor compositions comprising tetrahydrobenzotriazoles solubilized in activating solvents and methods for using same |
US9074289B2 (en) * | 2011-11-08 | 2015-07-07 | Nalco Company | Environmentally friendly corrosion inhibitor |
US20130310282A1 (en) | 2012-05-21 | 2013-11-21 | Halliburton Energy Services, Inc. | Wellbore Servicing Fluids and Methods of Making and Using Same |
CN103014715B (en) * | 2012-08-09 | 2014-09-10 | 江苏科技大学 | Corrosion inhibitor composition for preventing hydrogen sulfide corrosion |
WO2014136012A1 (en) | 2013-03-04 | 2014-09-12 | Schlumberger Technology B.V. | Corrosion inhibition |
WO2015084830A1 (en) | 2013-12-02 | 2015-06-11 | Ecolab Usa Inc. | Tetrazole based corrosion inhibitors |
CN103865506B (en) * | 2014-02-27 | 2017-01-11 | 山东泰和水处理科技股份有限公司 | High-temperature acidizing corrosion inhibitor for oil-gas fields and preparation method thereof |
GB2529723B (en) | 2014-09-01 | 2017-04-05 | Schlumberger Holdings | A method of corrosion inhibition of metal |
GB2537597A (en) | 2015-04-13 | 2016-10-26 | Schlumberger Holdings | Corrosion Inhibition |
GB2543498A (en) | 2015-10-19 | 2017-04-26 | Schlumberger Holdings | Corrosion inhibition |
-
2014
- 2014-12-05 GB GB1421656.8A patent/GB2532990A/en not_active Withdrawn
-
2015
- 2015-10-19 US US15/533,315 patent/US10787745B2/en active Active
- 2015-10-19 WO PCT/US2015/056144 patent/WO2016089487A1/en active Application Filing
- 2015-10-19 EP EP15864760.2A patent/EP3227470A4/en active Pending
- 2015-10-19 BR BR112017011894-7A patent/BR112017011894A2/en not_active Application Discontinuation
-
2017
- 2017-06-05 SA SA517381670A patent/SA517381670B1/en unknown
Also Published As
Publication number | Publication date |
---|---|
BR112017011894A2 (en) | 2018-07-03 |
WO2016089487A1 (en) | 2016-06-09 |
US20170335467A1 (en) | 2017-11-23 |
GB201421656D0 (en) | 2015-01-21 |
SA517381670B1 (en) | 2021-12-29 |
GB2532990A (en) | 2016-06-08 |
EP3227470A4 (en) | 2018-12-19 |
US10787745B2 (en) | 2020-09-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3227470A1 (en) | Corrosion inhibition | |
El Faydy et al. | Anticorrosion potential of some 5-amino-8-hydroxyquinolines derivatives on carbon steel in hydrochloric acid solution: gravimetric, electrochemical, surface morphological, UV–visible, DFT and Monte Carlo simulations | |
Wang | Inhibition of mild steel corrosion in phosphoric acid solution by triazole derivatives | |
US10059872B2 (en) | Corrosion inhibitor compositions for acidizing treatments | |
El Faydy et al. | Insight into the corrosion inhibition of new bis-quinolin-8-ols derivatives as highly efficient inhibitors for C35E steel in 0.5 M H2SO4 | |
Aiad et al. | Some imidazoline derivatives as corrosion inhibitors | |
Geng et al. | Rosin imidazoline as an eco-friendly corrosion inhibitor for the carbon steel in CO2-containing solution and its synergistic effect with thiourea | |
US10982337B2 (en) | Corrosion inhibition | |
WO2022152193A1 (en) | CORROSION INHIBITOR SUITABLE FOR ACIDIFICATION AT 200ºC AND USE THEREOF | |
WO2020082476A1 (en) | Preparation method for and use of dibenzylamine quaternary ammonium salt high-temperature resistant acidizing corrosion inhibitor | |
US10087530B2 (en) | Corrosion inhibition | |
Zhou et al. | Synthesis of Sulfobetaine‐type Zwitterionic Gemini surfactants (EAPMAC) and their oilfield application properties | |
Aly et al. | A newly synthesized sulphated 8-hydroxyquinoline derivative to effectively control aluminum corrosion in perchloric acid: Electrochemical and positron annihilation studies | |
GB2537597A (en) | Corrosion Inhibition | |
About et al. | A combined experimental and theoretical approach to the elucidation of the corrosion inhibition property of 5-((4, 5-dihydro-4-o-tolyltetrazol-1-yl) methyl) quinolin-8-ol for C22E steel in aggressive environment | |
CN112592705B (en) | Ecological safety type scale and corrosion inhibitor and preparation method thereof | |
US9758878B2 (en) | Mild steel corrosion inhibitor compounds | |
Al-Doori et al. | Study of Some [N-substituted] p-aminoazobenzene as Corrosion Inhibitors for Mild-Steel in 1M H2SO4 | |
CN105859626A (en) | Dithiocyanodiimidazoline bactericidal corrosion inhibitor, and preparation method and application thereof | |
US10844282B2 (en) | Corrosion inhibiting formulations and uses thereof | |
Frignani et al. | Inhibitors for Armco iron and ASTM A106 plain steel in hydrofluoric acid | |
Gao et al. | Some β-amino alcohols compounds as green volatile corrosion inhibitors for brass | |
US20170240796A1 (en) | Corrosion inhibition | |
US2836558A (en) | Method of inhibiting corrosion of metals | |
Al-Taq et al. | Performance of Synthesized Amine-based Corrosion Inhibitors in Concentrated HCl Acid Solutions: Effect of Intensifier |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE |
|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20170530 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
DAV | Request for validation of the european patent (deleted) | ||
DAX | Request for extension of the european patent (deleted) | ||
RIC1 | Information provided on ipc code assigned before grant |
Ipc: C09D 7/63 20180101ALI20180622BHEP Ipc: C09D 5/08 20060101ALI20180622BHEP Ipc: C23F 11/10 20060101ALI20180622BHEP Ipc: C23F 11/04 20060101AFI20180622BHEP Ipc: C23F 11/08 20060101ALI20180622BHEP Ipc: C09K 8/54 20060101ALI20180622BHEP Ipc: C23F 11/173 20060101ALI20180622BHEP Ipc: C23F 11/12 20060101ALI20180622BHEP Ipc: C23F 11/14 20060101ALI20180622BHEP Ipc: C23F 11/16 20060101ALI20180622BHEP |
|
A4 | Supplementary search report drawn up and despatched |
Effective date: 20181119 |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: C23F 11/10 20060101ALI20181113BHEP Ipc: C09D 5/08 20060101ALI20181113BHEP Ipc: C23F 11/14 20060101ALI20181113BHEP Ipc: C23F 11/173 20060101ALI20181113BHEP Ipc: C23F 11/08 20060101ALI20181113BHEP Ipc: C23F 11/04 20060101AFI20181113BHEP Ipc: C09K 8/54 20060101ALI20181113BHEP Ipc: C23F 11/12 20060101ALI20181113BHEP Ipc: C23F 11/16 20060101ALI20181113BHEP Ipc: C09D 7/63 20180101ALI20181113BHEP |